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首页> 外文期刊>Journal of Chemical Engineering of Japan >Hydrolysis of Methyl Acetate in Distillation Column Packed with Reactive Packing of Ion Exchange Resin
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Hydrolysis of Methyl Acetate in Distillation Column Packed with Reactive Packing of Ion Exchange Resin

机译:反应性填料离子交换树脂填充精馏塔中乙酸甲酯的水解

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References(7) Cited-By(47) Ion exchange resin tablets (7 mm diameter × 7 mm length) were molded from ion exchange resin beads and polyethylene powder in a furnace. 700 ml of the tablets was packed in a Pyrex glass tube of 36 mm diameter as a reaction zone and an Oldershaw column of 30 plates and 32 mm in diameter was employed as the recovery zone of the column. A mixture of methyl acetate and methanol (75:25 by weight) was fed to the bottom of the reaction zone at a rate of 89 g/h and water was fed to the top of the column at a rate of 89 g/h. When all the condensed top vapor was recycled at a rate of 254 g/h, the concentration of methyl acetate in the resulting reaction mixture discharged from the bottom was practically negligible.The reactive distillation column can be incorporated into the process of hydrolysis of methyl acetate for recovery of acetic acid and methyl alcohol. The advantages of the new process are the elimination of two columns in the conventional process and reduction of the heat requirement of the total process. The decrease in heat requirement is estimated to be about 50% that of the conventional process.
机译:参考文献(7)Cited-By(47)离子交换树脂片(直径7毫米×长度7毫米)由离子交换树脂珠和聚乙烯粉末在炉中模制而成。将700ml的片剂装填在直径为36mm的派热克斯玻璃管中作为反应区,并使用30个板且直径为32mm的Oldershaw柱作为该柱的回收区。将乙酸甲酯和甲醇的混合物(重量比为75:25)以89g / h的速度进料到反应区的底部,并将水以89g / h的速度进料到塔的顶部。当所有冷凝的塔顶蒸气以254 g / h的速度循环使用时,从塔底排出的反应混合物中乙酸甲酯的浓度几乎可以忽略不计。反应蒸馏塔可用于乙酸甲酯的水解过程用于回收乙酸和甲醇。新工艺的优点是在常规工艺中省去了两个塔,并减少了整个工艺的热量需求。热量需求的减少估计约为传统工艺的50%。

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